Heterogeneous Fenton-like degradation of 4-chlorophenol using iron/ordered mesoporous carbon catalyst

Ordered mesoporous carbon supported iron catalysts(Fe/OMC) were prepared by the incipient wetness impregnation method and investigated in Fenton-like degradation of 4-chlorophenol(4CP) in this work. XRD and TEM characterization showed that the iron oxides were well dispersed on the OMC support and grew bigger with the increasing calcination temperature. The catalyst prepared with a lower calcination temperature showed higher decomposition efficiency towards 4CP and H2O2, but more metals were leached. The effect of different operational parameters such as initial pH, H2O2 dosage, and reaction temperature on the catalytic activity was evaluated. The results showed that 96.1% of 4CP and 47.4% of TOC was removed after 270 min at 30°C, initial pH of 3 and 6.6 mmol/L H2O2. 88% of 4CP removal efficiency was retained after three successive runs, indicating Fe/OMC a stable catalyst for Fenton reaction. 4CP was degraded predominately by the attack of hydroxyl radical formed on the catalyst surface and in the bulk solution due to iron leaching. Based on the degradation intermediates detected by high performance liquid chromatography, possible oxidation pathways were proposed during the 4CP degradation.     

Combination of heterogeneous Fenton-like reaction and photocatalysis using Co-TiO2 nanocatalyst for activation of KHSO5 with visible light irradiation at ambient conditions

A novel coupled system using Co–Ti O2 was successfully designed which combined two different heterogeneous advanced oxidation processes, sulfate radical based Fenton-like reaction（SR-Fenton） and visible light photocatalysis（Vis-Photo）, for degradation of organic contaminants. The synergistic effect of SR-Fenton and Vis-Photo was observed through comparative tests of 50 mg/L Rhodamine B（Rh B） degradation and TOC removal. The Rhodamine B degradation rate and TOC removal were 100% and 68.1% using the SR-Fenton/Vis-Photo combined process under ambient conditions, respectively. Moreover, based on XRD, XPS and UV-DRS characterization, it can be deduced that tricobalt tetroxide located on the surface of the catalyst is the SR-Fenton active site, and cobalt ion implanted in the Ti O2 lattice is the reason for the visible light photocatalytic activity of Co–Ti O2. Finally, the effects of the calcination temperature and cobalt concentration on the synergistic performance were also investigated and a possible mechanism for the synergistic system was proposed. This coupled system exhibited excellent catalytic stability and reusability,and almost no dissolution of Co2＋was found.     

Herbicide Roundup® and its main constituents cause oxidative stress and inhibit acetylcholinesterase in liver of Carassius auratus

Roundup® is a glyphosate-based herbicide containing a mixture of surfactants. This paper evaluates the toxic effects of Roundup® and its main constituents on the goldfish, Carassius auratus, after 7 days exposure. Fish were exposed to 0.16, 0.032 and 0.0064 mg/L of Roundup® [containing 41% isopropylamine salt of glyphosate (G.I.S) and 18% polyoxyethylene amine (POEA)], G.I.S, and POEA. Their livers were taken for determining reactive oxygen species (ROS), superoxide dismutase (SOD) activity, malondialdehye (MDA) content and acetylcholinesterase (AChE) activity. Hydroxyl radical (·OH) could be induced by exposing Roundup® at a rate of 43%–111%, G.I.S at 90%–124% and POEA at142%–157%. A decreased SOD activity was observed in fish exposed to G.I.S and POEA. The contents of MDA significantly increased when exposed to Roundup® at all concentrations, 0.16 mg/L G.I.S and 0.032 mg/L POEA. The exposure led to an inhibition of AChE in livers overall during the experimental periods. POEA was more toxic than Roundup® or G.I.S during this experiment. AChE and ·OH are supposed to be sensitive biomarkers of the exposure of Roundup® and its main constituents to C. auratus.     

Aniline degradation by electrocatalytic oxidation

The degradation of aniline solution in alkaline medium of pH 11.0 by electrocatalytic oxidation has been studied using an electrochemical reactor containing a SnO₂–Sb₂O₃–PtO anode and a Ti cathode, both of 54 cm² area. Hydroxyl radicals (HO^√) are produced at the anode, being tested with the trace catcher salicylic acid and phenol by spectrophotometery and high performance liquid chromatography. Intermediates dianiline, 4-anilino phenol and azobenzol were detected by gas chromatography–mass spectrometry. The existence of HO^√ produced in the aniline degradation was assayed with scavenger tertiary butanol. The results showed that electrocatalytic oxidation is an effective process for the degradation of aniline. A general reaction pathway that accounts for aniline degradation to CO₂ involving those intermediates is proposed.     

高级氧化技术处理垃圾渗滤液的研究进展

本文介绍了包括化学氧化法、电化学氧化法、光催化氧化法、超声氧化法、辐照氧化法和催化湿式氧化法等在内的高级氧化技术的机理和运用于垃圾渗滤液处理的研究进展,并提出高级氧化技术与生物处理联合运用和各种高级氧化工艺之间的优化组合将是实现高级氧化技术在垃圾渗滤液处理中工程化运用的发展方向.     

石棉表面改性对石棉诱导人胚肺细胞产生羟基自由基的影响

为了研究用柠檬酸铝、混合稀土或亚硒酸钠预处理温石棉对石棉诱导人胚肺(HEL)细胞产生羟基自由基(·OH)的影响,笔者用不同浓度的柠檬酸铝、混合稀土或亚硒酸钠溶液浸泡温石棉1小时后,再将其与人胚肺细胞共同孵育,利用电子自旋捕获法测定反应体系中羟基自由基信号。结果显示,石棉可诱导人胚肺细胞产生羟基自由基,并且所产生的自由基信号(峰高)随石棉浓度升高而增强,呈一定的剂量依赖性。经3种化合物预处理的温石棉组人胚肺细胞所产生的自由基信号(峰高)均明显低于未处理温石棉组。上述结果表明,温石棉可诱导人胚肺细胞产生羟基自由基,但用3种化合物预处理温石棉,均可抑制温石棉诱导人胚肺细胞产生羟基自由基。     

电化学法生成Fenton试剂及其在工业染料废水降解脱色中的应用

以多孔石墨电极为阴极 ,电解时在阴极通以氧气或空气 ,电解生成的过氧化氢与阳极溶解的Fe2 +进行随后化学反应 ,现场生成羟基自由基 (Fenton试剂 ) ,进而对有机染整工业废水进行降解脱色反应。以可见光吸收谱图表征了工业染料废水经电解槽处理后吸光度的变化 ,以重铬酸钾法测试染料处理后的COD。实验结果表明 ,COD的去除率大于 80 % ,染料的脱色率达 1 0 0 % ,若将电解电流密度控制在 1 0mA/cm2 以下 ,槽电压可控制在 5V以内。实验结果表明 ,向阴极多孔石墨电极中通入空气与通入氧气的效果一致。     

溶液pH及电流浓度对电化学法生成羟基自由基降解机制的影响

用电化学稳态极化曲线分析方法讨论了溶液pH值及电流浓度对染料降解脱色的影响.实验结果表明,pH值将影响着阴极反应的方向、电极电位与染料降解脱色的效果.在酸性溶液中有利于过氧化氢的生成,阴极电位较低,但不利于随后的絮凝步骤;在中性溶液中染料降解脱色的综合效果较好,COD_Cr去除率可达80%以上.文中还讨论了电流浓度对降解脱色效果的影响,当电解槽内电流浓度达0.5 A/L时可取得满意的效果,电流浓度太大时,体系将伴随着析出氢气等的副反应,降解反应的电流效率下降.      

Comparison of UV/PDS and UV/H2O2 processes for the degradation of atenolol in water

UV/H2O2 and UV/peroxodisulfate (PDS) processes were adopted to degrade a typical β-blocker atenolol (ATL). The degradation efficiencies under various operational parameters (oxidant dosage, pH, HCO3-, humic acid (HA), NO3- , and Cl-) were compared. Principal factor analysis was also performed with a statistical method for the two processes. It was found that increasing the specific dosage of the two peroxides ([peroxide]0/[ATL]0 ) ranging from 1:1 to 8:1 led to a faster degradation rate but also higher peroxide residual. Within the pH range 3-11, the optimum pH was 7 for the UV/PDS process and elevating pH benefitted the UV/H 2O2 process. The presence of HCO3- , HA, and Cl adversely affected ATL oxidation in both processes. The NO3- concentration 1-3 mmol/L accelerated the destruction of ATL by the UV/PDS process, but further increase of NO3- concentration retarded the degradation process, contrary to the case in the UV/H2O2 process. The rank orders of effects caused by the six operational parameters were pH ≈ specific dosage > [HA]0 > [NO3-]0 > [HCO3-]0 > [Cl-]0 for the UV/H2O2 process and specific dosage > pH > [HA]0 > [NO3-]0 > [HCO3-]0 >[Cl-]0 for the UV/PDS process. The UV/PDS process was more sensitive to changes in operational parameters than the UV/H2O2 process but more efficient in ATL removal under the same conditions.